BACKGROUND OF THE INVENTIONThis invention relates to appartus in which conveyors transport materials through a liquid bath having two different temperature zones separated by a slotted wall. More particularly, the invention involves means for promoting the flow of liquid from one temperature zone through the slotted wall to the other zone.
U.S. Pat. No. 4,522,217 to D'Alterio shows in FIG. 4 a commercially successful form of liquid bath having two temperature zones in which a pair of continuous conveyor belts transport a pasta product through a zone of boiling water and through a slotted wall into and through a zone of cold water.
U.S. Pat. No. 2,286,644 to Pringle et al illustrates in FIG. 1 another apparatus in which conveyor belts carry potato slices through a cooking vat containing vegetable oil and having a slotted wall for the passage of the conveyor belts therethrough. The slotted wall thus permits the maintenance of different temperatures in the oil on its opposite sides.
In all such systems wherein a substantial temperature difference is desired in the zones of the liquid bath which are on opposite sides of a slotted wall, it is difficult to prevent the temperature of the liquid bath in the vicinity of the slot from being at some level intermediate the two desired zone temperatures. The aforesaid patent of D'Alterio discloses steam chests and containers filled with insulation adjacent the slot and on opposite sides of the wall in the liquid bath to minimize the amount of liquid bath which is not at either of the two desired zone temperatures. The suggested means for minimizing intermediate temperture near the slot are helpful but cumbersome both structurally and operationally.
A principal object of this invention is to provide simple and effective means for minimizing the amount or portion of liquid at less than desired temperature near the slot in a wall which divides a liquid bath into zones of different temperatures.
Another important object is to provide means for more positive control of liquid flow in the desired direction through the slotted wall in a liquid bath divided thereby into two different temperature zones.
A further important object is to provide means to scour the product on the conveyor passing through the slotted wall to loosen and remove undesirable matter from the product treated in the liquid bath.
These and other features and advantages of the invention will be apparent from the description which follows.
SUMMARY OF THE INVENTIONIn accordance with this invention, apparatus comprising continuous conveyor belts to transport a material while captured between belts through a liquid treating bath having two different temperature zones separated by a slotted wall through which the material is transported while submerged is provided with jets or nozzles that forcibly promote the flow of liquid from one temperature zone through the slotted wall to the other temperature zone of the liquid bath. In most cases, the higher temperature zone of the liquid bath has an appreciable loss of liquid through evaporation and, in such cases, make-up liquid is usually introduced from the lower temperature zone through the slotted wall. Hence, the jets of this invention are usually positioned and aimed to eject pressurized fluid streams through the slots in the wall into the higher temperature zone. The pressurized streams entrain liquid from the lower temperature zone through the wall slots into the higher temperature zone and thus facilitate positive liquid flow from one zone to the other in the desired direction.
While the liquid which forms the treating bath is in most cases used in the pressurized nozzles or jets, a gas or vapor may in some cases be the pressurized fluid ejected by the jets. For example, in the pasta cooking apparatus shown in FIG. 4 of U.S. Pat. No. 4,522,217, jets positioned in the cooling zone of the water bath could be used to eject streams of steam or hot pressurized air through the wall slots into the boiling water zone. The pressurized streams of steam or air would entrain water from the cooling zone through the wall slots into the boiling zone and thus enhance the desired water flow.
BRIEF DESCRIPTION OF THE DRAWINGSFor a fuller understanding of the invention, reference is made to the accompanying drawings of which:
FIG. 1 is a diagrammatic side elevation of a preferred system for treating a product conveyed through a liquid bath having two different temperature zones with conveyor belts extending from one zone through a slotted wall to the other zone wherein the nozzles of this invention are positioned in one zone to eject forceful fluid streams through the wall slots into the other zone;
FIG. 2 is similar to FIG. 1 and shows a different conveyor system in a liquid bath with two temperature zones having a slotted wall therebetween and equipped with the nozzles of this invention to shoot pressurized fluid streams through the wall slots;
FIG. 3 is an enlarged and more detailed representation of the portion of FIG. 1 showing the slotted wall and adjacent nozzles; and
FIG. 4 is like FIG. 3 but shows another embodiment of the nozzles of this invention.
DESCRIPTION OF PREFERRED EMBODIMENTSFIG. 1 is essentially a copy of FIG. 4 of U.S. Pat. No. 4,522,217 in which the nozzles of this invention have replaced the steam chests and containers filled with insulation shown in FIG. 4. Inasmuch as FIG. 4 is amply described in the patent, it will suffice to review only the principal elements of FIG. 1 herein.
In FIG. 1,tank 10 has an internal slottedwall 11 which dividestank 10 into two zones X,Y filled with the same liquid but maintained at different temperatures. Two mesh-type conveyor belts A,B have marginal openings which mesh with the teeth of drivensprockets 12. Belts A,B travel together in predetermined spaced relation frompoint 13 topoint 14. The product to be treated intank 10 is deposited on the portion of belt B above the liquid and becomes captured between belts A,B atpoint 13. After being transported through both zones X,Y of the liquid bath, the treated product is released by belt A atpoint 14 so that it can be removed from belt B.Internal wall 11 haswide slot 15 through which belts A,B and the product therebetween pass andnarrow slot 16 through which the return run of belt B passes.
In accordance with this invention,nozzles 17,18, 19,20 are positioned in zone Ynear wall 11 and aimed to discharge pressurized fluid streams throughslots 15,16 into zone X. The pressurized jet streams fromnozzles 17, 18,19,20 entrain liquid from zone Y throughslots 15,16 into zone X and provide a scouring action on both belts A, B and the product therebetween so that any adherent matter developed during the treatment of the product in zone X is loosened and removed therefrom.
The essential difference between FIG. 2 and FIG. 1 is the conveyor system.Tank 30 has slotted wall 31 which divides the liquid bath into zones X', Y' maintained at different temperatures. Three parallel, spacedconveyor belts 32 on drivensprockets 33 are immersed in zone X' and three parallel, spacedconveyor belts 34 on drivensprockets 35 are immersed in zone Y'.Long conveyor belt 36 on drivensprockets 37 extends from zone X' to zone Y' with its upper run passing throughwide slot 38 in wall 31 and its lower run passing throughnarrow slot 39 in wall 31.
Sprockets 33 oftop conveyor belt 32 in zone X' rotate counterclockwise,sprockets 33 of the nextlower belt 32 rotate clockwise,sprockets 33 of thelowest belt 32 rotate counterclockwise,sprockets 37 oflong belt 36 rotate clockwise,whilesprockets 35 oflowest belt 34 andtop belt 34 in zone Y' rotate counterclockwise andsprockets 35 ofmiddle belt 34 rotate clockwise. Therefore, product deposited onchute 40 is trapped between the lower run oftop belt 32 and the upper run ofmiddle belt 32 and conveyed to arcked guide orbaffle 41 where the product continues its travel in the reverse direction while held between the lower run ofmiddle belt 32 and the upper run ofbottom belt 32. Again atarcked guide 42, the product moves down to the upper run ofbelt 36 where together with the lower runs ofbottom belts 32,34 it is transported to arckedbaffle 43. There the product begins its upward progress through zone Y' by being carried between the top run ofbottom belt 34 and bottom run ofmiddle belt 34 to arcked guide 44 where the movement of the product is reversed by the top run ofmiddle belt 34 and the lower run oftop belt 34 until the treated product is pushed upinclined baffle 45 for removal from the system.
Pursuant to this invention,nozzles 46,47,48 are disposed in zone Y' near wall 31 with their orifices directed intoslots 38,39 so that pressurized fluid streams will entrain liquid from zone Y' into zone X' and effect a scouring action on the product as it passes onbelt 36 throughslot 38.
In the system of both FIG. 1 and FIG. 2, the conveyors carry the product to be treated along a zigzag path down through one zone of the liquid bath, through the slotted wall, and along a zigzag path up through the other zone. Hence, such conveyor arrangements can be tersely referred to as conveyors with zigzag travel; FIG. 1 has paired conveyor belts with zigzag travel, while FIG. 2 has multiple (more than two) conveyor belts with zigzag travel.
FIG. 3 shows on an enlarged scale the portion of FIG. 1 involving the lower part ofslotted wall 11 andnozzles 17,18,19,20. Conveyor belts A,B pass through wide,upper slot 15 ofwall 11, carrying therebetween the product undergoing treatment from zone X to zone Y of the liquid bath. The return run of belt B passes through narrow,lower slot 16 inwall 11 which meets the bottom oftank 10. Each ofnozzles 17,18,20 comprises aheader 17A,18A,20A, respectively, disposed near and parallel towall 11. The single nozzle appearing in FIG. 3 asnozzle 17 is actually a series of spaced, aligned nozzles attached toheader 17A with their orifices directed to shoot fluid streams intowall slot 15. Similarly, a series of spaced, alignednozzles 18 attached toheader 18A have their orifices directed towardslot 15. The series of spaced, alignednozzles 20 attached toheader 20A have their orifices directed to eject fluid streams into and throughwall slot 16.Header 19A has an upper series of spaced, aligned nozzles 19 with their orifices aimed intoupper wall slot 15 and a lower series of spaced, aligned nozzles 19 with their orifices aimed intolower wall slot 16.
Fluid supplied toheaders 17A,18A,19A,20A under pressure, e.g., 100 pounds per square inch, will issue as a multiplicity of high velocity jet streams entraining liquid from zone Y throughwall slots 15,16 into zone X of the liquid bath intank 10.Nozzles 17,18 will also exert a scrubbing action on conveyor belt A as well as the product therebelow carried on belt B while the upper series of nozzles 19 scrub belt B and the bottom of the product carried on belt B. Similarly, the lower series of nozzles 19 and the series ofnozzles 20 scrub conveyor belt B returning from zone Y to zone X of the liquid bath intank 10.
To minimize the amount of liquid in zone X which is not at its desired temperature as well as the amount of liquid in zone Y which is not at its desired different temperature, it is desirable to provide baffles extending fromslotted wall 11 to form a restricted channel to and/or fromslots 15,16. Thus,baffles 50,51 fastened towall 11 form a channel in zone X of the liquid bath communicating withslots 15,16. Baffles 52,53 on the opposite side ofwall 11 extend that channel in zone Y of the liquid bath. Either pair ofbaffles 50,51 or 52,53 helps to limit the amount of liquid not at its desired optimum temperature but both pairs ofbaffles 50,51 and 52,53 further limit the amount of liquid not at its desired temperature. It is evident that the channel formed bybaffles 50,51,52,53 is substantially linear and parallel to conveyor belts A,B passing therethrough.
FIG. 4 is similar to FIG. 3 but shows another embodiment of the nozzles of this invention. In this case, slottedwall 11 comprises three parallel and spacedducts 54,55,56, the space betweenducts 54,55 providingupper slot 15, and the space betweenducts 55,56 providinglower slot 16. The bottom wall ofduct 54 has two series of spaced, alignednozzles 57 with orifices disposed to eject pressurized fluid streams obliquely throughslot 15 into zone X of the liquid bath. Similarly, the top wall ofduct 55 has two series ofnozzles 58 with orifices aimed obliquely intoslot 15 while the bottom wall ofduct 55 has two series ofnozzles 59 with orifices set to send pressurized jet streams obliquely throughslot 16 into zone X. The top wall ofduct 56 likewise is provided with two series ofnozzles 60 with orifices aimed to shoot jet streams obliquely throughslot 16 into zone X.
The multiplicity of pressured streams fromnozzles 57,58 scrub conveyor belts A,B and the product carried therebetween throughslot 15 while the jet streams fromnozzles 59,60 likewise impinge obliquely on the return run of belt B passing throughslot 16 and effect scrubbing thereof.
The desirable option of forming an elongate channel leading to and/or fromslots 15,16 inwall 11 is illustrated by a pair ofparallel baffles 61,62 in zone X attached toducts 54,56, respectively, and a pair ofparallel baffles 63, 64 in zone Y also attached toducts 54,56, respectively.
In FIGS. 1 and 2,wall 11 has twoslots 15,16 for the passage of conveyor belts therethrough. However, when using the paired conveyor belts with zigzag travel of U.S. Pat. No. 4,522,217 it is possible to have only one slot in the wall between the two zones of the liquid bath. As illustrated by FIG. 1 of U.S. Pat. No. 4,522,217, the return run of belt B can be outside the liquid bath so that thelower slot 16 in FIG. 1 herein can be eliminated together withnozzles 20 and the lower series of nozzles 19.
As a specific example of the apparatus of FIG. 1 and FIG. 3 for cooking ravioli, metal mesh conveyor belts A,B are 161/2 inches wide and the spacing between them is 3/4 inch. Insulatedwall 11 is 4 inches wide andslots 15 and 16 measure vertically 13/8 inches and 3/8 inch, respectively.Headers 17A, 18A, 19A, 20A are pipes having an outside diameter of 1 inch and a wall thickness of 1/8 inch, and each header has its series of aligned nozzles spaced 3 inches from one another. The orifice of all the nozzles is 1/32 inch in diameter.Shields 50,51,52,53 individually extend from wall 11 a horizontal distance of 18 inches. Cool water at a temperature of 50° F. and a gauge pressure of 70 pounds per square inch issues as jet streams from the plurality ofnozzles 17,18,19,20 intowall slots 15,16 and the channel formed bybaffles 50,51 while entraining cool water from zone from zone Y through the channel formed bybaffles 52,53. The water jets fromnozzles 17,18 and upper 19 scrub the ravioli, loosening gelatinous starch on their surface and conveying the gelatinous matter into zone X so that the cool water in zone Y remains relatively clear and the ravioli discharged atpoint 14 have a glistening, clean appearance. The jets fromnozzles 17,18 and upper 19 also remove considerable heat stored in the ravioli and belts A,B leaving the boiling water in zone X through the channel formed bybaffles 50,51 so that the removed heat is carried back by the water into zone X rather than being dissipated in zone Y where the water is desirably maintained cold. If a different pasta product, e.g., lasagna ribbons, is processed in the apparatus of FIG. 1 and FIG. 3, the water pressure inheaders 17A,18A,19A,20A may be changed considerably depending on the weight of the product and speed of belts A,B. In most cases, the water gauge pressure is in the range of 10 to 100 pounds per square inch and the orifice diameter of the nozzles is usually in the range of about 0.020 to 0.125 inch. Also, as previously stated, steam or compressed air may be supplied toheaders 17A,18A,19A,20A instead of water.
Many variations and modifications of the invention will be apparent to those skilled in the art without departing from the spirit and scope of the invention. For instance,duct 54 withbaffles 61,63 of FIG. 4 may be used in FIG. 3 in lieu ofheaders 17A,18A, and baffles 50,52. Similarly,duct 56 withbaffles 62,64 of FIG. 4 may replaceheader 20A and baffles 51,53 in FIG. 3. While four baffles are shown in each of FIG. 3 and FIG. 4 to optimize the desired effects of the pressurized fluid streams directed through the slotted wall, the nozzles of this invention still benefit the operation of the two-zone bath without any baffle or with less than four baffles. For example, if the number of baffles is to be reduced in FIG. 4, for most operations baffle 64 may be eliminated in preference to baffle 63, and baffles 63,64 may be eliminated in preference tobaffles 61,62. Also, fornarrow slot 16 one set ofnozzles 59 or 60 may in some cases be adequate instead of using both sets ofnozzles 59 and 60. Accordingly, only such limitations should be imposed on the scope of the invention as are set forth in the appended claims.